[1] Corma A. From microporous to mesoporous molecular sieve materials and their use in catalysis [J]. Chemical Reviews, 1997, 97(6): 2373-2419.[2] Higgins J B, Lapierre R B, Schlenker J L, et al. The framework topology of zeolite-beta [J]. Zeolites, 1988, 8(6): 446-452. [3] Newsam J M, Treacy M M J, Koetsier W T, et al. Structural characterization of zeolite Beta [J]. Proceedings of the Royal Society of London Series, 1988, 420: 375-405. [4] Bellussi G, Pazzuconi G, Perego C, et al. Liquid-phase alkylation of benzene with light olefins catalyzed by β-zeolites [J]. Journal of Catalysis, 1995, 157(1): 227-234. [5] Ratnasamy P, Bhat R N, Pokhriyal S K, et al. Reactions of aromatic hydrocarbons over zeolite β [J]. Journal of Catalysis, 1989, 119(1): 65-70. [6] Pérez-Pariente J, Sastre E, Fornés V, et al. Isomerization and disproportionation of m-xylene over zeolite β [J]. Applied Catalysis, 1991, 69(1): 125-137. [7] 李丽,潘惠芳,李文兵.β沸石在烃类裂化催化剂中的应用[J].催化学报,2002,23(1):4 [8] 杜玥莹. 金属改性Beta分子筛材料对挥发性有机物的吸附和催化氧化性能研究[D].华南理工大学,2022.[9] 郭泉辉,李建伟,亢红霞等.铁改性分子筛直接催化分解一氧化二氮[J].化学反应工程与工艺,2007(04):337-342.[10] Jensen J C,Creyghton E J, Njo S L, et al. On the remarkable behaviour of zeolite Beta in acid catalysis[J]. Catalysis today,1997,38(2):205-212.[11] Kirsten L,et al. Impact of Copper Loading on NH3-Selective Catalytic Reduction, Oxidation Reactions and N2O Formation over Cu/SAPO-34[J]. Energies, 2017, 10(4)[12] 陈健.整体式β分子筛催化剂的成型及应用[D].北京化工大学,2014.[13] 缪赟,杨柳,王岚等.挤压成型催化剂的原料组分和表观形状研究进展[J]. 精细石油化工进展,2022,23(01):36-41.[14] 刘闪闪,丁其达,郭涛等.固定床催化剂成型工艺研究进展[J].过程工程学报,2023,23(04):501-511.[15] 华金铭,郑起,林性贻,等.整体式高温水煤气变换催化剂的初步研究[J].工业催化,2003,11( 3) : 16-20.[16] Box G,Wilson K B.On the experimental attainment of optimum conditions[J]. Journal of the Royal Statistical Society Series B: Statistical Methodology,1951( 1) : 1-45.[17 ] Mason R L,Gunst R F,Hess J L.Statistical design and analysis of experiments with applications to engineering and science[M].The United States of America: John Wiley and Sons Publication,2003.[18]K?l??, M., Pütün, E., Pütün, A.E., Optimization of euphorbia rigida fast pyrolysis conditions by using response surface methodology. [J]. Anal. Appl. Pyrolysis,2014(110):163-171[19]申明乐,陈海玲.拟薄水铝石的生产与应用[J].南阳理工学院学报,2009,1(04):67-70.[20] 张晓琳,王俊艳,曹志涛.分子筛催化剂成型条件对其抗压强度的影响[J].精细石油化工进展,2012,13(07):38-41.[21] 曹雨来,仇杨君,于泳,程亮,宋永吉,李翠清,王虹.催化分解N2O的催化剂工业中试应用条件研究[J].环境污染与防治,2018,40(01):80-83.[22] Junseong Ahn,Bongjae Kim,Sangho Lee. Fabrication Method of Zeolite Honeycomb Type Catalyst for Reducing Nitrogen Oxide[P]. United States Patent: US 8178063 B2,2012.[23] 刘国清,匡继刚,吴剑,等. 挤条成型 TS-1 分子筛催化剂制备及性能表征[J]. 化学反应工程与工艺,2010,26(1):42-46[24] 郭勤涛,张令弥,费庆国. 用于确定性计算仿真的响应面法及其试验设计研究[J]. 航空学报,2005,26( 1) : 55-61.[25] 王延克,丁渭平,杜飞龙,等. 基于响应面法的悬架结构改进及优化设计[J]. 机械科学与技术,2009,28( 1) : 10-14.[26] Ren W X,Chen H B. Finite element model updating in structural dynamics by using the response surface method[J].Engineering Structures,2010,32: 2455-2465.[27] X. Li, T. Lei, Z. Wang, X. Li, M. Wen, M. Yang, G. Chen, X. He, Q. Guan, Z. Li, Catalytic pyrolysis of corn straw with magnetic solid acid catalyst to prepare levulinic acid by response surface methodology [J]. Industrial Crops Products. 116 (2018): 73-80. |